Method for recovering cobalt from zinc-cobalt-nickel slag purified by zinc hydrometallurgy
A technology of hydrometallurgy and zinc purification, applied in the direction of improving process efficiency, etc., can solve problems such as difficult recovery of cobalt, achieve the effects of improving cobalt recovery rate, reducing unit consumption, and easy process control
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Embodiment 1
[0059] Purified zinc-cobalt-nickel slag is provided, the pre-leaching solution with an acid concentration of 250g / l is configured and heated to 85°C, and then the purified zinc-cobalt-nickel slag is added according to a liquid-solid mass ratio of 1:3 to carry out an acid leaching reaction. The reaction time of one acid leaching is 2 hours, and the acidity of the terminal system of the one acid leaching reaction is 0.2 g / l. After the completion of the one acid leaching reaction, filter is carried out to obtain the liquid after the first acid leaching and the residue of the first acid leaching.
[0060] Heat the pre-leaching solution with an acid concentration of 250g / l to 85°C, add the primary acid leaching residue according to the liquid-solid mass ratio of 5:1, and perform a secondary acid leaching reaction. The reaction of the secondary acid leaching reaction The time is 3 hours, the acidity of the system at the end point of the secondary acid leaching reaction is 17 g / l, and...
Embodiment 2
[0063] Purified zinc-cobalt-nickel slag is provided, the pre-leaching solution with an acid concentration of 200g / l is configured and heated to 85° C., and then the purified zinc-cobalt-nickel slag is added according to a liquid-solid mass ratio of 1:5 to carry out an acid leaching reaction. The reaction time of one acid leaching is 3 hours, and the acidity of the terminal system of the one acid leaching reaction is 1 g / l. After the completion of the one acid leaching reaction, it is filtered to obtain the liquid after the first acid leaching and the residue of the first acid leaching.
[0064] The pre-leaching solution with an acid concentration of 200g / l was heated to 85°C, and continued to add the primary acid leaching residue according to the liquid-solid ratio of 5:1 to carry out the secondary acid leaching reaction, and the secondary acid leaching reaction The reaction time is 2 hours, the acidity of the secondary acid leaching reaction terminal system is 5g / l, and the li...
Embodiment 3
[0067] Purified zinc-cobalt-nickel slag is provided, the pre-leaching solution with an acid concentration of 300g / l is configured and heated to 85°C, and then the purified zinc-cobalt-nickel slag is added according to a liquid-solid mass ratio of 1:2 to carry out an acid leaching reaction. The reaction time of one acid leaching is 3 hours, the pH of the system at the end of the first acid leaching reaction is 3.5, and after the completion of the first acid leaching reaction, filter to obtain the solution after the first acid leaching with a Co content of 6.18g / l.
[0068] Heat the solution after primary acid leaching with a Co content of 6.18g / l to 85°C, add ammonium salt which is 3 times the theoretically calculated amount, and carry out an oxidation reaction. The reaction time of the oxidation reaction is 5h, and after filtration, a Co 23% cobalt concentrate.
[0069] In summary, the present invention provides a method for recovering cobalt from zinc-cobalt-nickel slag purif...
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